EP1567560B1 - Organometallic transition metal compound, biscyclopentadienyl ligand system, catalyst system and process for preparing polyolefins - Google Patents

Organometallic transition metal compound, biscyclopentadienyl ligand system, catalyst system and process for preparing polyolefins Download PDF

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EP1567560B1
EP1567560B1 EP03785707A EP03785707A EP1567560B1 EP 1567560 B1 EP1567560 B1 EP 1567560B1 EP 03785707 A EP03785707 A EP 03785707A EP 03785707 A EP03785707 A EP 03785707A EP 1567560 B1 EP1567560 B1 EP 1567560B1
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Prior art keywords
ethanediylbis
zirconium dichloride
indenyl
radical
transition metal
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French (fr)
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EP1567560A1 (en
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Jörg SCHULTE
Jörg SCHOTTEK
Yoshikuni Okumura
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Basell Polyolefine GmbH
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Basell Polyolefine GmbH
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    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F17/00—Metallocenes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • B01J31/22—Organic complexes
    • B01J31/2282—Unsaturated compounds used as ligands
    • B01J31/2295—Cyclic compounds, e.g. cyclopentadienyls
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C13/00—Cyclic hydrocarbons containing rings other than, or in addition to, six-membered aromatic rings
    • C07C13/28—Polycyclic hydrocarbons or acyclic hydrocarbon derivatives thereof
    • C07C13/32—Polycyclic hydrocarbons or acyclic hydrocarbon derivatives thereof with condensed rings
    • C07C13/45—Polycyclic hydrocarbons or acyclic hydrocarbon derivatives thereof with condensed rings with a bicyclo ring system containing nine carbon atoms
    • C07C13/465—Indenes; Completely or partially hydrogenated indenes
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F110/04—Monomers containing three or four carbon atoms
    • C08F110/06—Propene
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
    • B01J2531/40—Complexes comprising metals of Group IV (IVA or IVB) as the central metal
    • B01J2531/48—Zirconium
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00—Polymerisation catalysts
    • C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
    • C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
    • C08F4/62—Refractory metals or compounds thereof
    • C08F4/64—Titanium, zirconium, hafnium or compounds thereof
    • C08F4/659—Component covered by group C08F4/64 containing a transition metal-carbon bond
    • C08F4/65912—Component covered by group C08F4/64 containing a transition metal-carbon bond in combination with an organoaluminium compound
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00—Polymerisation catalysts
    • C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
    • C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
    • C08F4/62—Refractory metals or compounds thereof
    • C08F4/64—Titanium, zirconium, hafnium or compounds thereof
    • C08F4/659—Component covered by group C08F4/64 containing a transition metal-carbon bond
    • C08F4/65916—Component covered by group C08F4/64 containing a transition metal-carbon bond supported on a carrier, e.g. silica, MgCl2, polymer
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S526/00—Synthetic resins or natural rubbers -- part of the class 520 series
    • Y10S526/941—Synthetic resins or natural rubbers -- part of the class 520 series having the transition metal bonded directly to carbon
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S526/00—Synthetic resins or natural rubbers -- part of the class 520 series
    • Y10S526/943—Polymerization with metallocene catalysts

Definitions

  • the present invention relates to organometallic transition metal compounds of the formula (I) Where
  • the present invention further relates to biscyclopentadienyl ligand systems having such a substitution pattern, catalyst systems comprising at least one of the organometallic transition metal compounds of the present invention, a process for preparing polyolefins by polymerization or copolymerization of at least one olefin in the presence of one of the catalyst systems of the present invention and the use of the biscyclopentadienyl ligand systems of the present invention for preparing organometallic transition metal compounds.
  • polyolefins based on ethylene and prepared by means of metallocene catalyst systems represent a dynamically growing market segment.
  • Variation of the substitution pattern on the ligand systems of ansa -metallocenes alters the steric circumstances around the active center and also its electronic structure. This makes it possible to influence, for example, the polymerization behavior of the catalyst constituents and also finally the properties of the polymers, e.g. isotacticity, chain length or molar mass and also the macroscopic materials properties of these polymers.
  • the catalyst system which usually comprises at least one organometallic transition metal compound and a cocatalyst component such as an aluminoxane, a strong Lewis acid or an ionic compound is generally used in supported form in order to avoid formation of deposits in the reactor.
  • EP 0 629 631 describes C 2 -symmetric 2,4,7-substituted ansa-metallocenes. It is demonstrated that the melting point of polypropylene prepared by means of such metallocenes is reduced compared to polypropylene which has been prepared using a corresponding C 2 -symmetrically 2,4-substituted ansa-metallocene. A significant influence of the substituents in the 7 position on the molecular weight of the polypropylenes was not observed.
  • WO 02/18397 describes an effective process for preparing highly substituted alkyl-bridged metallocenes.
  • the catalysts prepared using the metallocenes mentioned there give polypropylenes which do not have sufficiently high melting points.
  • the activity of the metallocenes to be discovered should not be inferior to that of the known metallocenes.
  • M 1 is an element of group 4 of the Periodic Table of the Elements, for example titanium, zirconium, hafnium, , preferably zirconium and hafnium, and particularly preferably zirconium.
  • the radicals X are identical or different, preferably identical, and are each halogen, for example fluorine, chlorine, bromine, iodine, preferably chlorine, hydrogen, C 1 -C 20 -, preferably C 1 -C 4 -alkyl, C 2 -C 20 -, preferably C 2 -C 4 -alkenyl, C 6 -C 22 -, preferably C 6 -C 10 -aryl, an alkylaryl or arylalkyl group having from 1 to 10, preferably from 1 to 4, carbon atoms in the alkyl part and from 6 to 22, preferably from 6 to 10, carbon atoms in the aryl part, -OR 6 or -NR 6 R 7 , preferably -OR 6 , where two radicals X may also be joined to one another, preferably two radicals -OR 6 which form, in particular, a substituted or unsubstituted 1,1'-di-2-phenoxide radical.
  • halogen for example fluorine,
  • Two radicals X can also form a substituted or unsubstituted diene ligand, in particular a 1,3-diene ligand.
  • the radicals R 6 and R 7 are each C 1 -C 10 -, preferably C 1 -C 4 -alkyl, C 6 -C 15 -, preferably C 6 -C 10 -aryl, alkylaryl, arylalkyl, fluoroalkyl or fluoroaryl each having from 1 to 10, preferably from 1 to 4, carbon atoms in the alkyl radical and from 6 to 22, preferably from 6 to 10, carbon atoms in the aryl radical.
  • the index n corresponds to the oxidation number of M 1 minus 2, and is 2 for the elements of group 4 of the Periodic Table of the Elements.
  • the radical R 1 is hydrogen or a C 1 -C 10 -alkyl radical.
  • radicals R 1 are hydrogen, methyl, ethyl, n-propyl, isopropyl, n-butyl, i-butyl, s-butyl, t-butyl, n-pentyl, cyclopentyl, n-hexyl, cyclohexyl, n-heptyl, n-octyl, in particular methyl, ethyl or isopropyl.
  • the radical R 2 is an unsubstituted or alkyl-substituted C 8 -C 40 -aryl radical having from 1 to 10, preferably from 1 to 4, carbon atoms in the alkyl part and from 6 to 22, preferably from 6 to 10, carbon atoms in the aryl part, with the radicals also being able to be halogenated.
  • R 2 examples of preferred radicals R 2 are phenyl, 2-tolyl, 3-tolyl, 4-tolyl, 2,3-dimethylphenyl, 2,4-dimethylphenyl, 2,5-dimethylphenyl, 2,6-dimethylphenyl, 3,4-dimethylphenyl, 3,5-dimethylphenyl, 3,5-di(tert-butyl)-phenyl, 2,4,6-trimethylphenyl, 2,3,4-trimethylphenyl, 1-naphthyl, 2-naphthyl, phenanthryl, p-isopropylphenyl, p-tert-butylphenyl, p-s-butylphenyl, p-cyclohexylphenyl and p-trimethylsilylphenyl.
  • the radical R 3 is hydrogen or a C 1 -C 10 -alkyl radical
  • examples of particularly preferred radicals R 3 are hydrogen, methyl, ethyl, n-propyl, isopropyl, n-butyl, i-butyl, s-butyl, t-butyl, n-pentyl, cyclopentyl, n-hexyl, cyclohexyl, n-heptyl, n-octyl, , in particular hydrogen, methyl, ethyl or isopropyl.
  • the radical R 4 is hydrogen or a C 1 -C 10 -alkyl radical.
  • Particular preferred radicals R 4 are hydrogen, methyl, ethyl, n-propyl, isopropyl, n-butyl, i-butyl, s-butyl, t-butyl, n-pentyl, cyclopentyl, n-hexyl, cyclohexyl, n-heptyl, n-octyl, in particular hydrogen, methyl, ethyl or isopropyl.
  • the radical R 5 is a C 1 -C 10 -alkyl radical.
  • radicals R 5 are methyl, ethyl, n-propyl, n-butyl, n-pentyl, n-hexyl, n-heptyl, n-octyl, in particular methyl or ethyl, very particularly preferably methyl.
  • alkyl encompasses linear or singly or multiply branched saturated hydrocarbons which may also be cyclic. Preference is given to a C 1 -C 18 -alkyl such as methyl, ethyl, n-propyl, n-butyl, n-pentyl, n-hexyl, n-heptyl, n-octyl, n-nonyl, n-decyl, cyclopentyl or cyclohexyl, isopropyl, isobutyl, isopentyl, isohexyl, sec-butyl or tert-butyl.
  • alkenyl as used in the present context encompasses linear or singly or multiply branched hydrocarbons having at least one C-C double bond. In the case of a plurality of C-C double bonds, these may be cumulated or may alternate.
  • aryl refers to aromatic and, possibly fused, polyaromatic hydrocarbon substituents which may be unsubstituted or monosubstituted or polysubstituted by linear or branched C 1 -C 18 -alkyl, C 1 -C 18 -alkoxy, C 2 -C 10 -alkenyl or C 3 -C 15 -alkylalkenyl.
  • substituted and unsubstituted aryl radicals are, in particular, phenyl, 4-methylphenyl, 4-ethylphenyl, 4-propylphenyl, 4-isopropylphenyl, 4-tert-butylphenyl, 4-methoxyphenyl, 1-naphthyl, 9-anthryl, 9-phenanthryl, 3,5-dimethylphenyl, 3,5-di-tert-butylphenyl and 4-trifluoromethylphenyl.
  • alkylalkenyl as used in the present context encompasses linear or singly or multiply branched hydrocarbons having one or more C-C double bonds which are isolated, so that the substituent has both alkyl and alkenyl sections.
  • arylalkyl refers to aryl-containing substituents whose aryl radical is linked to the appropriate part of the molecule via an alkyl chain.
  • Preferred examples are benzyl, substituted benzyl, phenethyl, substituted phenethyl and the like.
  • fluoroalkyl and fluoroaryl indicate that at least one hydrogen atom, preferably a plurality of and at most all hydrogen atoms, of the respective substituent are replaced by fluorine atoms.
  • fluorine-containing substituents which are preferred according to the present invention are trifluoromethyl, 2,2,2-trifluoroethyl, pentafluorophenyl, 4-trifluoromethylphenyl, 4-perfluoro-tert-butylphenyl and the like.
  • M 1 is preferably zirconium or hafnium, particularly preferably zirconium.
  • the radical R 1 is a C 1 -C 10 -alkyl radical, in particular a C 1 -C 4 -alkyl radical, very particularly preferably a methyl radical.
  • the radical R 3 is hydrogen or a C 1 -C 10 -alkyl radical, in particular hydrogen or a C 1 -C 4 -alkyl radical, very particularly preferably hydrogen or a methyl radical.
  • the radical R 4 is hydrogen or a C 1 -C 10 -alkyl radical, in particular hydrogen or a C 1 -C 4 -alkyl radical, very particularly preferably hydrogen or a methyl radical.
  • the radical R 5 is a C 1 -C 10 -alkyl radical, in particular a C 1 -C 4 -alkyl radical, very particularly preferably a methyl radical.
  • the novel organometallic transition metal compounds of the formula (I) give homopolymers, in particular isotactic polypropylene, having a melting point higher than that of homopolymers prepared using the previously known metallocenes having a related substitution pattern.
  • novel organometallic transition metal compounds of the formula (I) can be prepared by methods as described in WO 02/18397 .
  • the organometallic transition metal compounds of the formula (I) are usually obtained as a mixture of diastereomers, with the racemic isomer giving highly isotactic polypropylene while the corresponding, undesired diastereomer, viz. the meso form, usually gives atactic polypropylene.
  • the terms "meso” and “racemic” in the context of metallocenes are known and are defined, for example, in Rheingold et al. Organometallics 11 (1992), pages 1869-1876 .
  • organometallic transition metal compounds of the formula (I) can also be used as a mixture of diastereomers for the preparation of catalysts.
  • the invention further provides a biscyclopentadienyl ligand system of the formula (II) or its double bond isomers, where the variables R 1 , R 2 , R 3 , R 4 , R 5 and Z are as defined in formula (I).
  • the double bond isomers of the compound of the formula (II) result from a formal shift of one of the double bonds in the two five-membered rings.
  • the substitution pattern of the biscyclopentadienyl ligand systems of the formula (II) is decisive for the particular polymerization properties of the organometallic transition metal compounds in which these biscyclopentadienyl ligand systems are present.
  • the invention further provides for the use of a biscyclopentadienyl ligand system of the formula (II) for preparing an organometallic transition metal compound containing an element of group 4 of the Periodic Table of the Elements, in particular zirconium.
  • the present invention therefore also provides a process for preparing an organometallic transition metal compound, which comprises reacting a biscyclopentadienyl ligand system of the formula (II) or a bisanion prepared therefrom with a transition metal compound.
  • the usual procedure is firstly to doubly deprotonate a ligand system of the formula (II) by means of a base such as n-butyllithium and subsequently to react the product with a suitable transition metal source, for example zirconium tetrachloride.
  • the uncharged biscyclopentadienyl ligand system of the formula (II) can also be reacted directly with a suitable transition metal source having strongly basic ligands, for example tetrakis(dimethylamino)zirconium.
  • novel organometallic transition metal compounds of the formula (I) are highly active constituents of catalysts for the polymerization of olefins, particularly in the presence of suitable cocatalysts.
  • the present invention therefore also provides a catalyst system comprising at least one organometallic transition metal compound of the formula (I) and at least one cocatalyst.
  • the cocatalyst and the novel organometallic transition metal compound of the formula (I) together form a polymerization-active catalyst system in which the cocatalyst serves as cation-forming compound.
  • Suitable cation-forming compounds which are able to react with an organometallic transition metal compound according to the present invention to convert it into a cationic compound are, for example, compounds such as an aluminoxane, a strong uncharged Lewis acid, an ionic compound having a Lewis-acid cation or an ionic compound containing a Brönsted acid as cation.
  • the cation-forming compounds are frequently also referred to as compounds capable of forming metallocenium ions.
  • aluminoxanes it is possible to use, for example, the compounds described in WO 00/31090 .
  • Particularly useful compounds of this type are open-chain or cyclic aluminoxane compounds of the formula (III) or (IV) where
  • oligomeric aluminoxane compounds are usually prepared by reacting a solution of trialkylaluminum with water.
  • the oligomeric aluminoxane compounds obtained in this way are in the form of mixtures of both linear and cyclic chain molecules of different lengths, so that m is to be regarded as a mean.
  • the aluminoxane compounds can also be present in admixture with other metal alkyls, preferably aluminum alkyls.
  • modified aluminoxanes in which some of the hydrocarbon radicals or hydrogen atoms have been replaced by alkoxy, aryloxy, siloxy or amide groups can also be used in place of the aluminoxane compounds of the formula (III) or (IV).
  • the novel organometallic transition metal compound of the formula (I) and the aluminoxane compounds in such amounts that the atomic ratio of aluminum from the aluminoxane compounds to the transition metal from the organometallic transition metal compound is in the range from 10:1 1 to 1000:1, preferably in the range from 20:1 to 500:1 and in particular in the range from 30:1 to 400:1.
  • Strong uncharged Lewis acids which are suitable as cation-forming compounds also include the reaction products from the reaction of a boronic acid with two equivalents of a trialkylaluminum or the reaction products from the reaction of a trialkylaluminum with two equivalents of an acidic fluorinated, in particular perfluorinated, carbon compound such as pentafluorophenol or bis(pentafluorophenyl)borinic acid.
  • Suitable ionic compounds having Lewis-acid cations include salt-like compounds of the cation of the formula (VI) [(Y a+ )Q 1 Q 2 ...Q z ] d+ (VI) where
  • Particularly useful cations of this type are carbonium cations, oxonium cations and sulfonium cations and also cationic transition metal complexes. Particular mention may be made of the triphenylmethyl cation, the silver cation and the 1,1'-dimethylferrocenyl cation. They preferably have noncoordinating counterions, in particular boron compounds as are also mentioned in WO 91/09882 , preferably tetrakis(pentafluorophenyl)borate.
  • Salts having noncoordinating anions can also be prepared by combining a boron or aluminum compound, e.g. an aluminum alkyl, with a second compound which can react to link two or more boron or aluminum atoms, e.g. water, and a third compound which forms an ionizing ionic compound with the boron or aluminum compound, e.g. triphenylchloromethane.
  • a fourth compound which likewise reacts with the boron or aluminum compound e.g. pentafluorophenol, may be added.
  • Ionic compounds containing Brönsted acids as cations likewise preferably have noncoordinating counterions.
  • Brönsted acid particular preference is given to protonated amine or aniline derivatives.
  • Preferred cations are N,N-dimethylanilinium, N,N-dimethylcyclohexylammonium and N,N-dimethylbenzylammonium and also derivatives of the latter two.
  • Preferred ionic compounds as cation-forming compounds are, in particular, N,N-dimethylanilinium tetrakis(pentafluorophenyl)borate, N,N-dimethylcyclohexylammonium tetrakis(pentafluorophenyl)borate or N,N-dimethylbenzylammonium tetrakis(pentafluorophenyl)borate.
  • borate anions it is also possible for two or more borate anions to be joined to one another, as in the dianion [(C 6 F 5 ) 2 B-C 6 F 4 -B(C 6 F 5 ) 2 ] 2- , or the borate anion can be bound to the surface of a support particle via a bridge having a suitable functional group.
  • the amount of strong, uncharged Lewis acids, ionic compounds having Lewis-acid cations or ionic compounds containing Brönsted acids as cations is usually from 0.1 to 20 equivalents, preferably from 1 to 10 equivalents, per equivalent of the novel organometallic transition metal compound of the formula (I).
  • Further cation-forming compounds include boron-aluminum compounds such as di[bis(pentafluorophenyl)boroxy]methylalane. Boron-aluminum compounds of this type are disclosed, for example, in WO 99/06414 .
  • mixtures of all the abovementioned cation-forming compounds comprise aluminoxanes, in particular methylaluminoxane, and an ionic compound, in particular one containing the tetrakis(pentafluorophenyl)borate anion, and/or a strong uncharged Lewis acid, in particular tris(pentafluorophenyl)borane.
  • a solvent preferably an aromatic hydrocarbon having from 6 to 20 carbon atoms, in particular xylenes and toluene.
  • the catalyst may further comprise a metal compound of the formula (VII) M 3 (R 13 ) r (R 14 ) s (R 15 ) t (VII) where
  • Particularly preferred metal compounds of the formula (VII) are n-butyllithium, n-butyl-n-octylmagnesium, n-butyl-n-heptylmagnesium, tri-n-hexylaluminum, triisobutylaluminum, triethylaluminum and trimethylaluminum and mixtures thereof.
  • a metal compound of the formula (VII) is used, it is preferably present in the catalyst in such an amount that the molar ratio of M 3 from formula (VII) to transition metal M 1 from the novel organometallic transition metal compound of the formula (I) is from 800:1 to 1:1, in particular from 200:1 to 2:1.
  • a catalyst system comprising a novel organometallic transition metal compound of the formula (I) and at least one cocatalyst as cation-forming compound and further comprising a support.
  • the unsupported catalyst system can be reacted with a support.
  • the order in which the support, the organometallic transition metal compound according to the invention and the cocatalyst are combined is in principle immaterial.
  • the organometallic transition metal compound of the invention and the cocatalyst can be immobilized independently of one another or simultaneously.
  • the solid can be washed with suitable inert solvents such as aliphatic or aromatic hydrocarbons.
  • the support preference is given to using finely divided supports which can be any organic or inorganic, inert solids.
  • the support can be a porous solid such as talc, a sheet silicate, an inorganic oxide or a finely divided polymer powder (e.g. polyolefin).
  • Suitable inorganic oxides may be found among the oxides of the elements of groups 2, 3, 4, 5, 13, 14, 15 and 16 of the Periodic Table of the Elements.
  • oxides preferred as supports include silicon dioxide, aluminum oxide and mixed oxides of the elements calcium, aluminum, silicon, magnesium and titanium and also corresponding oxide mixtures.
  • Further inorganic oxides which can be used alone or in combination with the abovementioned preferred oxidic supports are, for example, MgO, ZrO 2 , TiO 2 or B 2 O 3 .
  • a preferred mixed oxide is, for example, calcined hydrotalcite.
  • the support materials used preferably have a specific surface area in the range from 10 to 1000 m 2 /g, a pore volume in the range from 0.1 to 5 ml/g and a mean particle size of from 1 to 500 ⁇ m.
  • Particular preference is given to supports having a specific surface area in the range from 200 to 400 m 2 /g, a pore volume in the range from 0.8 to 3.0 ml/g and a mean particle size of from 10 to 100 ⁇ m.
  • the inorganic support can be subjected to a thermal treatment, e.g. to remove adsorbed water.
  • a thermal treatment is generally carried out at from 80 to 300°C, preferably from 100 to 200°C, with drying at from 100 to 200°C preferably being carried out under reduced pressure and/or under a blanket of inert gas (e.g. nitrogen), or the inorganic support can be calcined at from 200 to 1000°C to generate, if appropriate, the desired structure of the solid and/or the desired OH concentration on the surface.
  • the support can also be treated chemically using customary desiccants such as metal alkyls, preferably aluminum alkyls, chlorosilanes or SiCl 4 or else methylaluminoxane. Suitable treatment methods are described, for example, in WO 00/31090 .
  • the inorganic support material can also be chemically modified.
  • treatment of silica gel with (NH 4 ) 2 SiF 6 leads to fluorination of the silica gel surface and treatment of silica gels with silanes containing nitrogen-, fluorine- or sulfur-containing groups leads to correspondingly modified silica gel surfaces.
  • Organic support materials such as finely divided polyolefin powders (e.g. polyethylene, polypropylene or polystyrene) can also be used and should preferably likewise be freed of adhering moisture, solvent residues or other impurities by appropriate purification and drying operations prior to use. It is also possible to use functionalized polymer supports, e.g. supports based on polystyrenes, via whose functional groups, for example ammonium or hydroxy groups, at least one of the catalyst components can be immobilized.
  • functionalized polymer supports e.g. supports based on polystyrenes, via whose functional groups, for example ammonium or hydroxy groups, at least one of the catalyst components can be immobilized.
  • At least one of the novel organometallic transition metal compounds of the formula (I) is brought into contact with at least one cocatalyst as cation-forming compound in a suitable solvent, preferably giving a soluble reaction product, an adduct or a mixture.
  • the preparation obtained in this way is then mixed with the dehydrated or passivated support material, the solvent is removed and the resulting supported organometallic transition metal compound catalyst system is dried to ensure that all or most of the solvent is removed from the pores of the support material.
  • the supported catalyst is obtained as a free-flowing powder. Examples of the industrial implementation of the above process are described in WO 96/00243 , WO 98/40419 or WO 00/05277 .
  • the cation-forming compound is firstly applied to the support component and this supported cation-forming compound is subsequently brought into contact with the organometallic transition metal compound of the present invention.
  • Cocatalyst systems of importance therefore likewise include combinations obtained by combining the following components: 1 st component: at least one defined boron or aluminum compound, 2nd component: at least one uncharged compound which possesses at least one acidic hydrogen atom, 3rd component: at least one support, preferably an inorganic oxidic support, and optionally as 4th component: a base, preferably an organic nitrogen-containing base, for example an amine, an aniline derivative or a nitrogen heterocycle.
  • the boron or aluminum compound used in the preparation of these supported cocatalysts are preferably compounds of the formula (VIII) where
  • Particularly preferred compounds of the formula (VIII) are trimethylaluminum, triethylaluminum and triisobutylaluminum.
  • the uncharged compounds which have at least one acidic hydrogen atom and can react with compounds of the formula (VIII) are preferably compounds of the formula (IX), (X) or (XI), where
  • Suitable compounds of the formula (IX) are water, alcohols, phenol derivatives, thiophenol derivatives or aniline derivatives, with halogenated and especially perfluorinated alcohols and phenols being of particular importance.
  • particularly useful compounds are pentafluorophenol, 1,1-bis(pentafluorophenyl)methanol and 4-hydroxy-2,2',3,3',4,4',5,5',6,6'-nonafluorobiphenyl.
  • Suitable compounds of the formula (X) include boronic acids and borinic acids, in particular borinic acids bearing perfluorinated aryl radicals, for example (C 6 F 5 ) 2 BOH.
  • Suitable compounds of the formula (XI) include dihydroxy compounds in which the divalent carbon-containing group is preferably halogenated, in particular perfluorinated.
  • An example of such a compound is 4,4'-dihydroxy-2,2',3,3',5,5',6,6'-octafluorobiphenyl hydrate.
  • Examples of combinations of compounds of the formula (VIII) with compounds of the formula (IX) or (XI) are trimethylaluminum/pentafluorophenol, trimethylaluminum/1-bis(pentafluorophenyl)methanol, trimethylaluminum-hydroxy-2,2',3,3',4,4',5,5',6,6'-nonafluorobiphenyl, triethylaluminum/pentafluorophenol and triisobutylaluminum/pentafluorophenol and triethylaluminum/4,4'-dihydroxy-2,2',3,3',5,5',6,6'-octafluorobiphenyl hydrate, with, for example, reaction products of the following type being able to be formed.
  • reaction products from the reaction of at least one compound of the formula (VIII) with at least one compound of the formula (X) are:
  • reaction products from the reaction of at least one compound of the formula (VIII) with at least one compound of the formula (IX), (X) or (XI) and optionally the organic nitrogen base are additionally combined with an organometallic compound of the formula (III), (IV), (V) and/or (VII) in order to then form the supported cocatalyst system on being combined with the support.
  • the 1 st component e.g. compounds of the formula (VIII)
  • the 2nd component e.g. compounds of the formula (IX), (X) or (XI)
  • a support as 3rd component and a base as 4th component are combined separately and subsequently reacted with one another, with the reaction preferably taking place in an inert solvent or suspension medium.
  • the supported cocatalyst formed can be freed of the inert solvent or suspension medium before it is reacted with the novel organometallic transition metal compound of the formula (I) and, if desired, a metal compound of the formula (VII) to form the catalyst system.
  • catalyst solid preferably linear C 2 -C 10 -1-alkenes, and in particular ethylene or propylene, and then to use the resulting prepolymerized catalyst solid in the actual polymerization.
  • the mass ratio of catalyst solid used in the prepolymerization to monomer polymerized onto it is usually in the range from 1:0.1 to 1:200.
  • an olefin preferably a ⁇ -olefin, for example vinylcyclohexane, styrene or phenyldimethylvinylsilane
  • an antistatic or a suitable inert compound such as a wax or oil
  • the molar ratio of additives to organometallic transition metal compound according to the present invention is usually from 1:1000 to 1000:1, preferably from 1:5 to 20:1.
  • the present invention also provides a process for preparing polyolefins by polymerization, i.e. homopolymerization or copolymerization, of at least one olefin in the presence of a catalyst system comprising at least one of the novel organometallic transition metal compounds of the formula (I).
  • the catalyst system is used together with a further metal compound of the formula (VII), which may be different from the metal compound or compounds of the formula (VII) used in the preparation of the catalyst system, for the polymerization or copolymerization of olefins.
  • the further metal compound is generally added to the monomer or the suspension medium and serves to free the monomer of substances which can adversely affect the catalyst activity. It is also possible for one or more additional cation-forming compounds to be added to the catalyst system in the polymerization process.
  • the olefins can be functionalized, olefinic unsaturated compounds such as esters or amide derivatives of acrylic or methacrylic acid, for example acrylates, methacrylates or acrylonitrile, or be nonpolar olefinic compounds, including aryl-substituted ⁇ -olefins.
  • olefins examples include 1-olefins having from 2 to 40, preferably from 2 to 10, carbon atoms, e.g. ethylene, propylene, 1-butene, 1-pentene, 1-hexene, 1-heptene, 1-octene, 1-decene or 4-methyl-1-pentene or unsubstituted or substituted vinylaromatic compounds such as styrene and styrene derivatives, or dienes such as 1,3-butadiene, 1,4-hexadiene, 1,7-octadiene, 5-ethylidene-2-norbornene, norbornadiene, ethylnorbornadiene or cyclic olefins such as norbornene, tetracy-clododecene or methylnorbornene.
  • 1-olefins having from 2 to 40, preferably from 2 to 10, carbon atoms, e.g. ethylene, prop
  • the catalyst system of the present invention is particularly preferably used for homopolymerizing propylene or ethylene or copolymerizing ethylene with C 3 -C 8 - ⁇ -olefins such as propylene, 1-butene, 1-pentene, 1-hexene and/or 1-octene and/or cyclic olefins such as norbornene and/or dienes having from 4 to 20 carbon atoms, e.g. 1,4-hexadiene, norbornadiene, ethylidenenorbornene or ethylnorbornadiene or, particularly preferably, copolymerizing propylene with ethylene and/or 1-butene.
  • C 3 -C 8 - ⁇ -olefins such as propylene, 1-butene, 1-pentene, 1-hexene and/or 1-octene and/or cyclic olefins such as norbornene and/or dienes having from 4 to 20 carbon
  • copolymers obtained in this way are propylene-ethylene, propylene-1-butene, ethylene-1-butene, ethylene-1-hexene and ethylene-1-octene copolymers, and ethylene-propylene-ethylidenenorbornene and ethylene-propylene-1,4-hexadiene terpolymers.
  • the polymerization can be carried out in a known manner in bulk, in suspension, in the gas phase or in a supercritical medium in the customary reactors used for the polymerization of olefins. It can be carried out batchwise or preferably continuously in one or more stages. Solution processes, suspension processes, stirred gas-phase processes or gas-phase fluidized-bed processes are all possible. As solvent or suspension medium, it is possible to use inert hydrocarbons, for example isobutane, or else the monomers themselves.
  • the polymerization can be carried out at from -60 to 300°C and pressures in the range from 0.5 to 3000 bar. Preference is given to temperatures in the range from 50 to 200°C, in particular from 60 to 100°C and pressures in the range from 5 to 100 bar, in particular from 15 to 70 bar.
  • the mean residence times are usually from 0.5 to 5 hours, preferably from 0.5 to 3 hours.
  • Hydrogen can be used in the polymerization as molar mass regulator and/or to increase the activity. It is also possible to use customary additives such as antistatics.
  • the catalyst system of the present invention can be used directly for the polymerization, i.e. it is introduced in pure form into the polymerization system, or it is admixed with inert components such as paraffins, oils or waxes in order to improve the meterability.
  • novel organometallic transition metal compounds of the formula (I) and the catalyst systems in which they are present are especially useful for preparing propylene homopolymers having high melting points.
  • the polymers prepared by the process of the present invention are, in particular, suitable for producing strong, hard and stiff shaped bodies such as fibers, filaments, injection-molded parts, films, sheets or large hollow bodies (e.g. pipes).
  • the melting point T m was determined by means of DSC measurement in accordance with ISO standard 3146 in a first heating phase at a heating rate of 20°C per minute to 200°C, a dynamic crystallization at a cooling rate of 20°C per minute to 25°C and a second heating phase at a heating rate of 20°C per minute to 200°C once again. The melting point was then the temperature at which the curves of the enthalpy versus the temperature measured in the second heating phase displayed a maximum.
  • the solvent was removed completely under reduced pressure and the residue, viz. 2.5 g of crude complex, was admixed with 150 ml of toluene at 80°C. After filtration through a layer of Celite, the toluene solution was evaporated to about 8 ml and admixed with 5 ml of n-heptane. A solid precipitated at -30°C and this was filtered off, analyzed by NMR and then discarded. The filtrate was once again evaporated completely, dissolved in 30 ml of toluene/5 ml of heptane at 100°C and an insoluble residue was filtered off once again.
  • Example 2 was repeated, but 1,2-Et(2-Me-4-( p - t Bu-Ph)-1-Ind) 2 ZrCl 2 was used in place of the metallocene from example 1 for preparing the catalyst in this experiment.
  • Example 2 was repeated, but 1,2-Et(2,4,7-Me 3 -1-Ind) 2 ZrCl 2 was used in place of the metallocene from example 1 for preparing the catalyst in this experiment.
  • the homopolymerization was carried out in a 5 I reactor charged with 3 I of liquid propene.
  • the reactor had been made inert by means of nitrogen before being charged.
  • 2.4 ml of a 20% strength by weight solution of triethylaluminum in Exsol (from Witco) were added to the propene in the reactor and the mixture was stirred at 30°C for 15 minutes.
  • a suspension of 500 mg of the catalyst prepared in example 2 in 20 ml of Exsol was introduced into the reactor.
  • the reactor temperature was increased to 65°C and the reactor was maintained at this temperature for 60 minutes.
  • the polymerization was stopped by venting the reactor.
  • the polymer was dried overnight under reduced pressure.
  • the results of the polymerization and the results of the analysis of the polymer are shown in the table below.
  • the homopolymerization was carried out in a 2 I reactor charged with 1.5 I of liquid propene.
  • the reactor had been made inert by means of nitrogen before being charged.
  • 1.7 ml of a 20% strength by weight solution of triethylaluminum in Exsol (from Witco) were introduced into the reactor and the mixture was stirred at 30°C for 15 minutes.
  • a suspension of 600 mg of the catalyst prepared in comparative example A in 20 ml of Exsol was introduced into the reactor.
  • the reactor temperature was increased to 65°C and the reactor was maintained at this temperature for 60 minutes.
  • the polymerization was stopped by venting the reactor.
  • the polymer was dried overnight under reduced pressure.

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EP03785707A 2002-12-06 2003-12-02 Organometallic transition metal compound, biscyclopentadienyl ligand system, catalyst system and process for preparing polyolefins Expired - Lifetime EP1567560B1 (en)

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DE10257332 2002-12-06
DE10257332A DE10257332A1 (de) 2002-12-06 2002-12-06 Organoübergangsmetallverbindung, Biscyclopentadienylligandsystem, Katalysatorsystem und Verfahren zur Herstellung von Polyolefinen
US44459503P 2003-02-03 2003-02-03
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